US7144561B2 - Method for the preparation of iron hydroxide, iron oxide hydrate or iron oxide from filter salts of dilute acid recovery - Google Patents
Method for the preparation of iron hydroxide, iron oxide hydrate or iron oxide from filter salts of dilute acid recovery Download PDFInfo
- Publication number
- US7144561B2 US7144561B2 US10/745,693 US74569303A US7144561B2 US 7144561 B2 US7144561 B2 US 7144561B2 US 74569303 A US74569303 A US 74569303A US 7144561 B2 US7144561 B2 US 7144561B2
- Authority
- US
- United States
- Prior art keywords
- iron oxide
- solution
- iron
- hydroxide
- filter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related, expires
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G49/00—Compounds of iron
- C01G49/02—Oxides; Hydroxides
- C01G49/06—Ferric oxide [Fe2O3]
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G49/00—Compounds of iron
- C01G49/02—Oxides; Hydroxides
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S423/00—Chemistry of inorganic compounds
- Y10S423/01—Waste acid containing iron
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S423/00—Chemistry of inorganic compounds
- Y10S423/01—Waste acid containing iron
- Y10S423/02—Sulfuric acid
Definitions
- the invention relates to a method for the preparation of iron hydroxide, iron oxyhydrate or iron oxide from filter salts of dilute acid recovery.
- Dilute acid consists essentially of dilute sulfuric acid which contains the dissolved salts (mainly iron salts).
- the latter is concentrated and filter salts, or green salts, are produced, which are separated.
- the filter salts are thus produced in large amounts and, on account of their accompanying components they cannot easily be used industrially, but have to be disposed of, often at great expense.
- the invention is addressed to the problem of overcoming the disadvantages of the state of the art and especially to create a process whereby iron hydroxide or iron oxide with a content of >90 wt.-% of Fe 2 O 3 can be recovered from the filter salts of dilute acid recovery.
- the problem is solved by a method for the preparation of iron oxide, iron oxide hydrate or iron oxide for filter salts of dilute acid recovery wherein the filter salts are dissolved in water, the solution is adjusted to a pH of ⁇ 1, preferably ⁇ 0.5, then by adding a strong base with stirring a pH of 2 to 4, preferably 3 to 3.8, the substances then precipitating are separated in a known manner, the remaining solution is adjusted with the addition of a strong base and/or an oxidizing agent to a pH of 6 to 8, the precipitating iron hydroxide or iron oxide hydrate is separated from the solution, washed, dried and if necessary dried and/or calcined to iron oxide.
- the filter salt solution already has a pH of ⁇ 1 and then does not have to be adjusted separately. Otherwise, sulfuric acid or dilute acid is used for the adjustment of the pH.
- the filter salt solution contains preferably 200 to 350 g of solid matter per kg of solution.
- An alkali metal hydroxide solution is used preferably as the strong base; caustic soda solution or caustic potash solution is especially preferred.
- the substances precipitating at a pH of 2 to 4 contain mainly metatitanic acid. Preferably, this is fed back into the titanium dioxide process.
- Air, oxygen or hydrogen peroxide (H 2 O 2 ) is used preferably as oxidant. When air or oxygen are used they are blown into the solution.
- the calcining or drying temperature amounts preferably to 200 to 1300° C., especially preferably 300 to 1300° C., and quite especially preferably 600 to 1200° C.
- the calcining or drying can also be performed under vacuum.
- the advantage of the method of the invention is that high-quality iron hydroxide or iron oxide hydrate and, after calcining, iron oxide with a content of >90 wt-% Fe 2 O 3 is obtained.
- the washing of the precipitated iron hydroxide is preferably repeated until the electrical conductivity in the washing filtrate is under 200 ⁇ S/cm ⁇ 1 especially preferably under 150 ⁇ S/cm ⁇ 1 In this manner an iron oxide is obtained after calcining, with a content of 94 wt-% Fe 2 O 3 .
- an aqueous filter salt solution was prepared. This solution had a pH of 0. This means that sufficient acid was adhering to the filter salts, so that a separate addition of acid was unnecessary.
- the temperature of the solution was about 23° C.
- the solution was adjusted by stirring with about 150 ml of 50% caustic soda solution to a pH of 3.5, the temperature of the solution increasing to 55° C. After a 2-hour maturation phase at about 40° C. the precipitated solids were separated from the filtrate with a suction filter. The filtrate cooled during the solid-liquid separation to about 25° C.
- the filter solution was then again adjusted with 180 ml of 50% NaOH, with turbulent stirring during which atmospheric oxygen went into the solution, to a pH of 7.8, when much iron hydroxide precipitated.
- the iron hydroxide was dried in the dryer for 12 hours and then calcined for 2 hours at 600° C. in a laboratory oven in atmospheric air.
- the iron oxide obtained had a content of 94.5% Fe 2 O 3 .
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Iron (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10232069A DE10232069A1 (de) | 2002-07-16 | 2002-07-16 | Verfahren zur Herstellung von Eisenhydroxid, Eisenoxidhydrat oder Eisenoxid aus Filtersalzen der Dünnsäurerückgewinnung |
| DE10232069.1 | 2002-07-16 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| US20050019250A1 US20050019250A1 (en) | 2005-01-27 |
| US7144561B2 true US7144561B2 (en) | 2006-12-05 |
Family
ID=29761981
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US10/745,693 Expired - Fee Related US7144561B2 (en) | 2002-07-16 | 2003-07-08 | Method for the preparation of iron hydroxide, iron oxide hydrate or iron oxide from filter salts of dilute acid recovery |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US7144561B2 (de) |
| EP (1) | EP1382571B1 (de) |
| JP (1) | JP2004051477A (de) |
| DE (2) | DE10232069A1 (de) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090145856A1 (en) * | 2007-12-11 | 2009-06-11 | Raymond Letize A | Acid recycle process with iron removal |
| CN104843799A (zh) * | 2015-04-12 | 2015-08-19 | 耿兆翔 | 氧化铁粉末中粉末氧化铝或/和氧化钙的分离回收方法 |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6960201B2 (en) * | 2002-02-11 | 2005-11-01 | Quanticum, Llc | Method for the prevention and treatment of skin and nail infections |
| DE102004031181A1 (de) * | 2004-06-28 | 2006-01-19 | Vifor (International) Ag | Phosphatadsorbens |
| WO2008106576A1 (en) * | 2007-02-28 | 2008-09-04 | Keraderm Llc | Phototherapy treatment and device to improve the appearance of nails and skin |
| US20240024357A1 (en) * | 2020-09-29 | 2024-01-25 | Chien-Chin Wu | Methods of preparing iron complexes |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3619137A (en) * | 1969-01-16 | 1971-11-09 | Pfizer | Production of iron oxide pigments |
| US3816593A (en) * | 1971-11-30 | 1974-06-11 | W Massey | Method of regenerating waste pickle liquor |
| US3927173A (en) * | 1974-02-22 | 1975-12-16 | Armco Steel Corp | Treatment of acid waste waters to produce ferromagnetic sludges |
| US4119536A (en) * | 1974-09-05 | 1978-10-10 | Nippon Electric Co., Ltd. | Method of disposing of a ferrous-ion containing acidic aqueous waste by forming polycrystalline iron compound particles |
| US4889697A (en) * | 1987-12-10 | 1989-12-26 | Nkk Corporation | Method of refining ferrous ion-containing acid solution |
| US5785862A (en) * | 1994-03-04 | 1998-07-28 | Imperial College Of Science Technology & Medicine | Preparation and uses of polyferric sulphate |
| US6139753A (en) * | 1997-03-21 | 2000-10-31 | Geo2 Limited | Method for treating acidic waste water |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3016286A (en) * | 1960-02-29 | 1962-01-09 | Ishihara Sangyo Kaisha | Method for the treatment of waste acid resulting from titanium dioxide production |
| DE2331569A1 (de) * | 1972-06-29 | 1974-01-17 | Oceanic Process Corp | Verfahren zur behandlung verbrauchter, saurer beizfluessigkeit |
| JPH01208331A (ja) * | 1988-02-15 | 1989-08-22 | Sumitomo Metal Ind Ltd | フェライト用酸化鉄の製造方法 |
| DE4235947A1 (de) * | 1992-10-23 | 1994-04-28 | Bayer Ag | Farbreine Eisenoxid-Direktrotpigmente, Verfahren zu ihrer Herstellung sowie deren Verwendung |
| DE19746262A1 (de) * | 1997-10-20 | 1999-04-22 | Bayer Ag | Eisenoxidrotpigmente, Verfahren zur Herstellung von Eisenoxidrotpigmenten und deren Verwendung |
| DE19812261A1 (de) * | 1998-03-20 | 1999-09-23 | Bayer Ag | Verfahren zur Aufarbeitung von Dünnsäure aus der TiO¶2¶-Herstellung |
| DE19812260A1 (de) * | 1998-03-20 | 1999-09-23 | Bayer Ag | Verfahren zur Herstellung von Eisenoxid-Pigmenten aus Dünnsäure aus der TiO¶2¶-Herstellung |
-
2002
- 2002-07-16 DE DE10232069A patent/DE10232069A1/de not_active Withdrawn
-
2003
- 2003-07-08 US US10/745,693 patent/US7144561B2/en not_active Expired - Fee Related
- 2003-07-09 EP EP03015714A patent/EP1382571B1/de not_active Expired - Lifetime
- 2003-07-09 DE DE50302037T patent/DE50302037D1/de not_active Expired - Lifetime
- 2003-07-14 JP JP2003196654A patent/JP2004051477A/ja not_active Ceased
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3619137A (en) * | 1969-01-16 | 1971-11-09 | Pfizer | Production of iron oxide pigments |
| US3816593A (en) * | 1971-11-30 | 1974-06-11 | W Massey | Method of regenerating waste pickle liquor |
| US3927173A (en) * | 1974-02-22 | 1975-12-16 | Armco Steel Corp | Treatment of acid waste waters to produce ferromagnetic sludges |
| US4119536A (en) * | 1974-09-05 | 1978-10-10 | Nippon Electric Co., Ltd. | Method of disposing of a ferrous-ion containing acidic aqueous waste by forming polycrystalline iron compound particles |
| US4889697A (en) * | 1987-12-10 | 1989-12-26 | Nkk Corporation | Method of refining ferrous ion-containing acid solution |
| US5785862A (en) * | 1994-03-04 | 1998-07-28 | Imperial College Of Science Technology & Medicine | Preparation and uses of polyferric sulphate |
| US6139753A (en) * | 1997-03-21 | 2000-10-31 | Geo2 Limited | Method for treating acidic waste water |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090145856A1 (en) * | 2007-12-11 | 2009-06-11 | Raymond Letize A | Acid recycle process with iron removal |
| WO2009075710A1 (en) * | 2007-12-11 | 2009-06-18 | Macdermid, Incorporated | Acid recycle process with iron removal |
| CN104843799A (zh) * | 2015-04-12 | 2015-08-19 | 耿兆翔 | 氧化铁粉末中粉末氧化铝或/和氧化钙的分离回收方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| DE50302037D1 (de) | 2006-02-02 |
| JP2004051477A (ja) | 2004-02-19 |
| US20050019250A1 (en) | 2005-01-27 |
| DE10232069A1 (de) | 2004-02-05 |
| EP1382571B1 (de) | 2005-12-28 |
| EP1382571A1 (de) | 2004-01-21 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: SACHTIELBEN CHEMIE GMBH, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:GOSCH, BODO;REEL/FRAME:015145/0237 Effective date: 20030801 |
|
| AS | Assignment |
Owner name: SACHTLEBEN CHEMIE GMBH, GERMANY Free format text: REEL/FRAME 015145/0237-ASSIGNEE 1ST NAME MISSPELLED;ASSIGNOR:GOSCH, BODO;REEL/FRAME:018422/0728 Effective date: 20030801 |
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| FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
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| FPAY | Fee payment |
Year of fee payment: 4 |
|
| REMI | Maintenance fee reminder mailed | ||
| LAPS | Lapse for failure to pay maintenance fees | ||
| STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |
|
| FP | Lapsed due to failure to pay maintenance fee |
Effective date: 20141205 |